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  • 1
    In: Journal of Power Sources, Elsevier BV, Vol. 247 ( 2014-02), p. 1026-1032
    Type of Medium: Online Resource
    ISSN: 0378-7753
    Language: English
    Publisher: Elsevier BV
    Publication Date: 2014
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  • 2
    In: Journal of Power Sources, Elsevier BV, Vol. 245 ( 2014-01), p. 1-6
    Type of Medium: Online Resource
    ISSN: 0378-7753
    Language: English
    Publisher: Elsevier BV
    Publication Date: 2014
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  • 3
    Online Resource
    Online Resource
    The Electrochemical Society ; 2013
    In:  Journal of The Electrochemical Society Vol. 160, No. 8 ( 2013), p. A1181-A1186
    In: Journal of The Electrochemical Society, The Electrochemical Society, Vol. 160, No. 8 ( 2013), p. A1181-A1186
    Type of Medium: Online Resource
    ISSN: 0013-4651 , 1945-7111
    RVK:
    Language: English
    Publisher: The Electrochemical Society
    Publication Date: 2013
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  • 4
    Online Resource
    Online Resource
    The Electrochemical Society ; 2014
    In:  ECS Meeting Abstracts Vol. MA2014-02, No. 5 ( 2014-08-05), p. 439-439
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2014-02, No. 5 ( 2014-08-05), p. 439-439
    Abstract: Introduction Safety is more important than high energy in stationary batteries. In addition, material choices based on the low-cost and easy production of larger batteries is another critical issue for developing large energy storage systems comparable to pumped hydro systems. A solvent-free solid polymer electrolyte (SPE) has the advantages of being safe, inexpensive and barrier-free for large battery production. However, polyether-based SPEs are believed to oxidize at 〉 4 V. Carbon-based anodes are also thought to be incompatible with polyether-based SPEs. Therefore, such SPEs are now in categorized as traditional electrolytes. However, we demonstrated (i) the compatibility of 4 V-5 V cathodes, such as LiCoO 2 1) and LiNi 0.5 Mn 1.5 O 4 2) , by modifying the cathode and polyether-based SPE interface and (ii) sufficient graphite reversibility with the SPE using suitably prepared electrodes. Recently, we drastically improved the cycle operation ( 〉 1,500 cycles) of LiNi 1/3 Mn 1/3 Co 1/3 O 2 (NMC) 3) and graphite using an optimized lithium salt and by introducing carboxymethylcellulose (CMC) at the interface. These materials are already mass produced; therefore, the active material cost will be equivalent to conventional lithium-ion batteries. There are no flammable vapors in the electrolyte (a pure polymer rather than a gel); therefore, an intrinsic safety improvement is expected for abused cells. In addition, a simple, multi-cell design using one external package is another advantage of all solid state batteries. Based on these advantages and renovations, we readopted such traditional SPE systems for stationary batteries. Here, we further improved the cycle performance by adding a new lithium salt and demonstrated the long term operation of a [Graphite | SPE | NMC] × 3 stack 12 V single-package multi-cell. Experimental The electrode materials were mixed with CMC, styrene-butadiene rubber (SBR) and conductive additives in a solvent without any SPEs before coating on the current collector. Subsequently, a polyether-based SPE ( M =1.5 M, Daiso Co., Ltd.) was overcoated on the electrode using acetonitrile (AN). LiBF 4 was used in the overcoat solution for NMC. In contrast, LiTFSI was used in the overcoat solution for graphite and the SPE sheet between the two electrodes. A lithium-ion cell composed of NMC, SPE, and graphite was fabricated using an Al-laminate-type cell. For the multi-cell, three cells (effective surface area 10 ×10 cm) were stacked in series in one package. All cells operated at 50°C. Results and Discussion We added 5 % LiBOB to the NMC overcoat solution. This LiBOB additive remarkably improved the reversibility, as shown in Fig. 1. The LiBOB additive was reported to suppress Al corrosion and/or Mn dissolution. While the detailed mechanism for these improvements is currently being studied, the high retention capacity obtained (70 % at 3,000 cycles) is practical for stationary use. Furthermore, over 1,000 operating cycles were successfully performed using a 10×10 cm three stack 12 V multi-cell, as shown in Fig. 2. The stacked multi-cell was vacuum sealed so no additional pressure was required during operations, which is significant progress for a large format battery design. References Y. Kobayashi et al., Journal of Power Sources, 146, 719 (2005). H. Miyashiro et al., Electrochem. Commun., 7, 1083 (2005). T. Kobayashi et al., ACS Applied Materials & Interfaces, 5, 12387 (2013). H. Xie et al., Electrochem. Solid State Lett., 11, C19 (2008). M. Xu et al., J. Electrochem. Soc., 160, A2005 (2013).
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2014
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  • 5
    Online Resource
    Online Resource
    The Electrochemical Society ; 2013
    In:  ECS Meeting Abstracts Vol. MA2013-01, No. 4 ( 2013-03-08), p. 148-148
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2013-01, No. 4 ( 2013-03-08), p. 148-148
    Abstract: Abstract not Available.
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2013
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  • 6
    In: The Journal of Dermatology, Wiley, Vol. 51, No. 3 ( 2024-03)
    Type of Medium: Online Resource
    ISSN: 0385-2407 , 1346-8138
    URL: Issue
    RVK:
    Language: English
    Publisher: Wiley
    Publication Date: 2024
    detail.hit.zdb_id: 2222121-9
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  • 7
    In: Journal of Power Sources, Elsevier BV, Vol. 295 ( 2015-11), p. 162-166
    Type of Medium: Online Resource
    ISSN: 0378-7753
    Language: English
    Publisher: Elsevier BV
    Publication Date: 2015
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  • 8
    Online Resource
    Online Resource
    The Electrochemical Society ; 2016
    In:  ECS Meeting Abstracts Vol. MA2016-03, No. 2 ( 2016-06-10), p. 1004-1004
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2016-03, No. 2 ( 2016-06-10), p. 1004-1004
    Abstract: Introduction Li-rich oxides, Li(Li x Me 1- x )O 2 (Me = Co, Ni, Mn), are promising positive electrode active materials for lithium-ion cells because of their ability to deliver capacities over 250 mAhg -1 .[1, 2]  However, the mechanisms responsible for their unique voltage profiles, such as the activation voltage plateau in the 1 st delithiation cycle and voltage hysteresis during cycling, are not fully understood. Electrochemical calorimetry is a powerful tool to observe reversible / irreversible reactions during charge and discharge of the electrode. In addition, the observed reversible heat flow can be described in terms of the change in configurational entropy of lithium ions (D S ) in the structure, the heat of polarization, and side reactions. D S is also obtained using the temperature dependence of the open circuit voltage ( dE/dT ). Here, we compare the heat flow during charge and discharge, open circuit voltage (OCV), and dE/dT to evaluate reversible and irreversible reaction factors of the Li-rich oxides. Experimental All data reported here are obtained on the cathode material denoted as Li(Li 0.2 Ni 0.15 Mn 0.55 Co 0.1 )O 2 = (0.5Li 2 MnO 3 - 0.5LiNi 0.375 Co 0.25 Mn 0.375 O 2 ). Coin-type half cells containing c.a. 10 mg cathode material with counter lithium metal were prepared, and the heat flow during charge and discharge was observed using an isothermal microcalorimeter. We also measured OCV and dE/dT at every 2.5 % state of charge (SOC), and correlated the values to the obtained heat flow. In the case of OCV assumption, the relaxation time of OCV (t) was also determined. Results and Discussion As is well known, the lithium-rich oxide material shows the wide voltage plateau only during the 1 st cycle.[3] We observed a large gap between the 1 st cycle charge voltage and OCV (Figure 1(a)) and also large exothermic heat in the corresponding region (capacity 〉 100 mAhg -1 ) as shown in Figure 1(b). dE/dT values are negative (which means endothermic reaction during charge as shown in Figure 1(b); £). The estimated total heat flow (red dots), taking into consideration the heat of polarization from OCV (Figure 1(b); ) is obviously lower than the observed heat flow (blue line). This observation suggests large irreversible exothermic heat flow for oxide capacities 〉 100 mAhg -1 . In addition, the relaxation time constant (Figure 1(c); °) also drastically increases in the corresponding region, which suggests that the irreversible reactions are slower than the reversible reactions. The heat flow during the 2 nd charge cycle is distinctly different from that of the 1 st cycle. However, the gap between observed heat flow (blue line in Figure 1 (e)) and the estimated one from dE/dT and heat of polarization (Figure 1 (e); ) remained, which indicates the persistence of irreversible reactions. These irreversible heat flows may be associated with the energy required to induce structural changes within the oxide particles. In our presentation we will discuss the origins of the oxide voltage hysteresis using the heat flow, dE/dT , OCV, and the OCV relaxation times (t) obtained from the charge and discharge cycles. Figure 1
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2016
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  • 9
    Online Resource
    Online Resource
    The Electrochemical Society ; 2016
    In:  ECS Meeting Abstracts Vol. MA2016-03, No. 2 ( 2016-06-10), p. 202-202
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2016-03, No. 2 ( 2016-06-10), p. 202-202
    Abstract: Introduction  Large scale Lithium-ion batteries are starting to be installed in the world to stabilize the voltage and frequency because variable powers such as photovoltaic and wind powers are installed for the electrical power systems. Life-time estimation is very important for maintenance of batteries and degradation analysis is developed to contribute to this estimation.  We have developed the degradation analysis of small size cells by using cell disassembly and reproduction of cells [1, 2]. Misalignment of the operational area of the positive and negative electrodes in the cell due to the lithium irreversible consumption at the anode mainly occurred in the degrade cells.  In this study, we investigate the degradation behavior of large size lithium-ion batteries with several ten Ah. Experimental  30Ah class commercial cells were tested in this study. Galvanostatically cycle test were performed in the 10-90% SOC range during charge and discharge at 25, 35 and 45 degC. The other cells were charged up to 50%, 70% and 100% SOC at 25 degC and stored at 25, 35 and 45 degC. The test intervals are 80 and 120 cycle at cycle test and 15 and 20 days at storage one. Capacity test were performed in C/20 rate at 25degC among the cycle and starage test period. Temperature test was conducted using the original thermal insulator. Postmortem analysis were performed at cycled and SOC 50% aged sells at 45degC. These cells were disassembled in an Ar globe box and reassembled to coin cells. Capacity tests were performed in C/20 rate with half-cells and “Nico-ichi” cell with quasi-reference electrode. Results and Discussion  The cells were analyzed by the results of the differential voltage versus capacity, dV/dQ vs. Q analysis using “Nico-ichi” coin cell and temperature measurement during charge and discharge using a quasi-adiabatic cell folder. It was observed that dV/dQ peaks and temperature peaks shifted with decreasing cell capacity as shown in Fig.1. The analysis of peak shifts has potentials to the non-destructive prediction of the cell life. References 1. Y. Kobayashi, T. Kobayashi, K. Shono, Y. Ohno, Y. Mita and H. Miyashiro, J. Electrochem. Soc., 160 (2013) A1181 – A1186. 2. K. Shono, T. Kobayashi, M. Tabuchi, Y. Ohno, H. Miyashiro and Y. Kobayashi, J. Power Sources, 247 (2014) 1026 – 1032. Figure 1
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2016
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  • 10
    Online Resource
    Online Resource
    The Electrochemical Society ; 2010
    In:  ECS Meeting Abstracts Vol. MA2010-02, No. 11 ( 2010-07-08), p. 1116-1116
    In: ECS Meeting Abstracts, The Electrochemical Society, Vol. MA2010-02, No. 11 ( 2010-07-08), p. 1116-1116
    Abstract: Abstract not Available.
    Type of Medium: Online Resource
    ISSN: 2151-2043
    Language: Unknown
    Publisher: The Electrochemical Society
    Publication Date: 2010
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